JP2008511656A5 - - Google Patents

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JP2008511656A5
JP2008511656A5 JP2007530277A JP2007530277A JP2008511656A5 JP 2008511656 A5 JP2008511656 A5 JP 2008511656A5 JP 2007530277 A JP2007530277 A JP 2007530277A JP 2007530277 A JP2007530277 A JP 2007530277A JP 2008511656 A5 JP2008511656 A5 JP 2008511656A5
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cta
representative sample
ppmw
particles
composition
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JP2007530277A
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JP2008511656A (ja
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Priority claimed from US11/154,219 external-priority patent/US7683210B2/en
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JP2007530277A 2004-09-02 2005-08-29 粗製テレフタル酸組成物及びその製造方法 Pending JP2008511656A (ja)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US60680804P 2004-09-02 2004-09-02
US63134604P 2004-11-29 2004-11-29
US11/154,219 US7683210B2 (en) 2004-09-02 2005-06-16 Optimized liquid-phase oxidation
PCT/US2005/030857 WO2006028818A1 (en) 2004-09-02 2005-08-29 Crude terephthalic acid composition and production process thereof

Publications (2)

Publication Number Publication Date
JP2008511656A JP2008511656A (ja) 2008-04-17
JP2008511656A5 true JP2008511656A5 (enExample) 2008-11-20

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JP2007530277A Pending JP2008511656A (ja) 2004-09-02 2005-08-29 粗製テレフタル酸組成物及びその製造方法

Country Status (10)

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US (3) US7683210B2 (enExample)
EP (2) EP2251315A1 (enExample)
JP (1) JP2008511656A (enExample)
KR (1) KR101281248B1 (enExample)
CN (1) CN101010282B (enExample)
BR (1) BRPI0514781A (enExample)
CA (1) CA2576799A1 (enExample)
MX (2) MX344104B (enExample)
PL (1) PL1784378T3 (enExample)
WO (1) WO2006028818A1 (enExample)

Families Citing this family (19)

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US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7919652B2 (en) 2005-05-19 2011-04-05 Eastman Chemical Company Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone
US7834208B2 (en) 2005-05-19 2010-11-16 Eastman Chemical Company Process to produce a post catalyst removal composition
US7432395B2 (en) * 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
US7741516B2 (en) 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US7880031B2 (en) 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
US7897809B2 (en) 2005-05-19 2011-03-01 Eastman Chemical Company Process to produce an enrichment feed
US7884231B2 (en) 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
US7557243B2 (en) 2005-05-19 2009-07-07 Eastman Chemical Company Enriched terephthalic acid composition
US7304178B2 (en) 2005-05-19 2007-12-04 Eastman Chemical Company Enriched isophthalic acid composition
US7888529B2 (en) 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US20100113735A1 (en) 2008-10-31 2010-05-06 Eastman Chemical Company Integrated Co-Production of Dicarboxylic Acids
US9505692B2 (en) * 2008-10-31 2016-11-29 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with self-fuel oxidative destruction
US9493387B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with minimal wastewater generation
US9493389B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with enhanced energy recovery
US9493388B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with direct fired off-gas heating
US9849434B2 (en) * 2010-09-22 2017-12-26 Grupo Petrotemex, S.A. De C.V. Methods and apparatus for enhanced gas distribution
US20160264511A1 (en) * 2015-03-13 2016-09-15 Grupo Petrotemex, S.A. De C.V. Bubble column reactor based digester and method for its use

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